JP4411250B2 - Method for producing tea beverage - Google Patents

Method for producing tea beverage Download PDF

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JP4411250B2
JP4411250B2 JP2005193174A JP2005193174A JP4411250B2 JP 4411250 B2 JP4411250 B2 JP 4411250B2 JP 2005193174 A JP2005193174 A JP 2005193174A JP 2005193174 A JP2005193174 A JP 2005193174A JP 4411250 B2 JP4411250 B2 JP 4411250B2
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tea beverage
nitrogen
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正巳 笹目
謙次 島岡
洋子 原口
泉 小林
和芳 西村
英男 野村
憲一 阿部
哲也 大貫
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株式会社 伊藤園
株式会社日本キヤンパック
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本発明は、茶飲料の製造方法に関し、より詳細には、優れた香気を有する茶飲料を製造する方法に関する。   The present invention relates to a method for producing a tea beverage, and more particularly to a method for producing a tea beverage having an excellent aroma.

茶飲料の製造工程では、茶抽出液の酸化による劣化をいかに抑制するかが重要な課題である。よって、酸素を遮断するための様々な方法が考えられてきた。例えば、脱気水を用いて抽出を行う方法が提案されている。しかしながらこの方法では、抽出以後の工程で酸素が再溶存し得るために、安定した効果が得られないという課題がある。また、抽出水から強制的に酸素を脱気すると、茶葉のジャンピング効果が失われるという問題もあった。   In the manufacturing process of tea beverages, how to suppress deterioration due to oxidation of tea extract is an important issue. Thus, various methods for blocking oxygen have been considered. For example, a method of performing extraction using deaerated water has been proposed. However, this method has a problem that a stable effect cannot be obtained because oxygen can be redissolved in the steps after extraction. In addition, when oxygen is forcibly degassed from the extracted water, there is a problem that the jumping effect of tea leaves is lost.

その他の方法として、特許文献1には、炭酸ガスにより脱気する方法が記載されている。しかしながら、炭酸ガスは水溶液への溶解性が高いために、完全に溶液中から除去することが難しい。炭酸ガスの脱気が不十分であると、炭酸ガスによる酸味が残り、風味に影響する。また、炭酸ガスを脱気する工程で溶液中から香気が発散し、茶飲料としての香気が弱まるという問題があった。   As another method, Patent Document 1 describes a method of degassing with carbon dioxide gas. However, since carbon dioxide has high solubility in an aqueous solution, it is difficult to completely remove it from the solution. If the degassing of carbon dioxide is insufficient, the sourness due to carbon dioxide remains and affects the flavor. Further, in the process of degassing the carbon dioxide gas, there is a problem that the fragrance is emitted from the solution and the fragrance as a tea beverage is weakened.

特許文献2には、窒素雰囲気下で飲料を製造する方法が記載されている。しかし、この方法では、溶液中への酸素の溶解を防ぐだけであり、元々溶液中に存在している酸素濃度を下げることは出来ない。また、特許文献3には、乳性飲料などの製造において、窒素等の不活性ガスで置換して液中溶存酸素5 ppm以下にすることにより、加熱によって発生するジメチルジサルファイドの発生を減少させる方法が記載されている。しかしながら、茶飲料は色調の変化や香気の変化が起こりやすいため、単に窒素を混合することにより酸化劣化を抑制する方法では、茶飲料として提供し得る製品にすることは難しかった。
特許第3452805号 特開2002−211676 特許第3083798号
Patent Document 2 describes a method for producing a beverage under a nitrogen atmosphere. However, this method only prevents the dissolution of oxygen in the solution, and cannot reduce the oxygen concentration originally present in the solution. Patent Document 3 discloses that in the production of dairy beverages, the generation of dimethyl disulfide generated by heating is reduced by substituting with an inert gas such as nitrogen so that the dissolved oxygen in the liquid is 5 ppm or less. A method is described. However, since tea beverages tend to change in color and aroma, it has been difficult to produce products that can be provided as tea beverages by a method that suppresses oxidative degradation by simply mixing nitrogen.
Japanese Patent No. 3452805 JP2002-211676 Japanese Patent No. 3083798

上記問題に鑑み、本発明は、茶飲料の酸化劣化による香味の損失を抑制し、品質的に安定し且つ香味の優れた茶飲料を製造する方法を提供することを目的とする。   In view of the above problems, an object of the present invention is to provide a method for producing a tea beverage that suppresses flavor loss due to oxidative degradation of a tea beverage, is stable in quality, and has an excellent flavor.

本発明に拠れば、茶葉を抽出し、得られた茶抽出液をpH5.0〜6.0に調整する工程と、該茶抽出液に窒素を混合し、0.01 MPa以上の負圧を加える工程と、前記負圧を加える工程に続いて、該茶抽出液を大気圧以下の圧力下で30秒〜20分間維持し、安定化させる工程と、前記安定化工程中又は該工程後に、該茶抽出液をpH5.5〜6.5に調整する工程と、を具備する、茶飲料の製造方法が提供される。ここで、前記安定化工程後にpHを調整された茶抽出液は、溶存酸素量が1 ppm以下であることが好ましい。また、前記安定化工程は大気圧下で行われることが好ましい。   According to the present invention, extracting tea leaves, adjusting the obtained tea extract to pH 5.0 to 6.0, mixing nitrogen into the tea extract, and applying a negative pressure of 0.01 MPa or more, Following the step of applying the negative pressure, the tea extract is maintained at a pressure below atmospheric pressure for 30 seconds to 20 minutes for stabilization, and the tea extract during or after the stabilization step. And a step of adjusting the pH to 5.5 to 6.5. Here, the tea extract whose pH is adjusted after the stabilization step preferably has a dissolved oxygen content of 1 ppm or less. Moreover, it is preferable that the said stabilization process is performed under atmospheric pressure.

さらに、前記茶飲料を殺菌し、密封容器に充填する工程が具備さる。好ましくは該充填工程は無菌条件下で行われる。また、前記密封容器は、高バリアPETであることが好ましい。   Furthermore, the process which sterilizes the said tea drink and fills a sealed container is comprised. Preferably, the filling step is performed under aseptic conditions. The sealed container is preferably high barrier PET.

本発明に拠れば、茶飲料の製造工程における酸化劣化を抑制することが可能であり、品質的に安定し且つ優れた香味及び色調を有する容器詰茶飲料を製造することが可能である。   According to the present invention, it is possible to suppress oxidative deterioration in the production process of a tea beverage, and it is possible to produce a packaged tea beverage that is stable in quality and has an excellent flavor and color.

本発明は、香味及び色調の優れた茶飲料、好ましくは容器詰茶飲料を製造する方法である。本発明者らは、茶抽出液が熱により酸化促進される点に着目し、製造工程中で最も熱負荷がかかり溶存酸素の影響を受けやすい殺菌工程に先立って、液中の溶存酸素濃度を低減させておくことにより、香味に優れた茶飲料を提供することを可能とした。   The present invention is a method for producing a tea beverage excellent in flavor and color, preferably a containerized tea beverage. The inventors pay attention to the fact that the tea extract is accelerated by heat, and prior to the sterilization process that is most susceptible to the influence of dissolved oxygen due to the most heat load in the production process, the dissolved oxygen concentration in the liquid is determined. By reducing it, it was possible to provide a tea beverage with excellent flavor.

本発明では、液中の溶存酸素濃度を低減させる方法として窒素を混合させる方法を用いる。しかし、緑茶飲料は性状が変化しやすく、この方法を行った場合に色調や香気が劣化してしまうという問題があった。本発明者らは、この窒素混合による影響がpHの上昇に起因することを明らかにし、pHを制御することによって窒素の影響を抑制することに成功した。   In the present invention, a method of mixing nitrogen is used as a method of reducing the dissolved oxygen concentration in the liquid. However, the nature of green tea beverages is likely to change, and there is a problem that the color tone and aroma deteriorate when this method is used. The present inventors have clarified that the influence of this nitrogen mixing is caused by an increase in pH, and succeeded in suppressing the influence of nitrogen by controlling the pH.

本発明の茶飲料の製造方法では、まず茶葉を抽出して茶抽出液を調製する。茶葉の抽出方法は周知の方法で行えばよく、茶葉の種類や目的とする茶飲料製品の特徴等によって、抽出温度や抽出時間等の条件を適宜選択してよい。茶葉を抽出した後、茶葉と液分を分離し、冷却する。次いで、液分をろ過し、清澄な茶抽出液を得る。この茶抽出液は任意に希釈してよい。   In the method for producing a tea beverage of the present invention, tea leaves are first extracted to prepare a tea extract. The extraction method of tea leaves may be performed by a well-known method, and conditions such as extraction temperature and extraction time may be appropriately selected according to the type of tea leaves and the characteristics of the target tea beverage product. After extracting the tea leaves, the tea leaves and the liquid are separated and cooled. Next, the liquid is filtered to obtain a clear tea extract. This tea extract may be optionally diluted.

次いで、得られた茶抽出液のpHを5.0〜6.0の範囲、好ましくは5.3〜5.8の範囲に調整する。後の工程において窒素を混合する際に、pH6.0以上では液色の褐変、劣化臭の発生が生じ、また、pH5.0未満ではイモ臭といわれる香気が発生し、さらにクリームダウンが生じる恐れがある。本発明の方法に従って、pHを5.0〜6.0の範囲にすることにより、香味性状の劣化を防ぐことができる。好ましくは5.3〜5.8の範囲にすることにより、香味性状の劣化をさらに最小限に防ぐことができる。pHの調整は、周知の適切な添加物を用いて行えばよく、例えばアスコルビン酸、重曹等を用いてよいが、これらに限定されない。   Next, the pH of the obtained tea extract is adjusted to a range of 5.0 to 6.0, preferably 5.3 to 5.8. When mixing nitrogen in the subsequent process, liquid color browning and generation of deteriorated odor occur at pH 6.0 or higher, and odor called potato odor occurs at pH less than 5.0, which may further cause cream down There is. According to the method of the present invention, the deterioration of flavor properties can be prevented by adjusting the pH to the range of 5.0 to 6.0. By making it preferably in the range of 5.3 to 5.8, the deterioration of flavor properties can be further prevented to a minimum. The pH may be adjusted using a known appropriate additive, for example, ascorbic acid, sodium bicarbonate, etc., but is not limited thereto.

次に、pHを調整した茶抽出液に窒素を混合する。窒素の混合は周知の方法に従って行えばよく、例えばガス置換方式で行うことができる。次いで、窒素を混合した後、速やかに0.01 MPa以上の負圧を加える。即ち、0.01 MPa以上のマイナスの差圧を生じさせる。0.01 MPa以上のマイナスの差圧を加えることによって、窒素の混合分散が促進され、窒素を溶液に安定的に分散させることができ、酸素濃度を効率的に軽減することが可能である。また、負圧を加える程度は0.01 MPa以上であれば特に限定されないが、発泡の観点から1MPaを限度とし、更には0.5MPa以下であることが好ましい。   Next, nitrogen is mixed with the tea extract whose pH is adjusted. Nitrogen may be mixed according to a well-known method, for example, gas replacement. Next, after mixing nitrogen, a negative pressure of 0.01 MPa or more is immediately applied. That is, a negative differential pressure of 0.01 MPa or more is generated. By applying a negative differential pressure of 0.01 MPa or more, the mixing and dispersion of nitrogen is promoted, nitrogen can be stably dispersed in the solution, and the oxygen concentration can be efficiently reduced. Further, the degree to which the negative pressure is applied is not particularly limited as long as it is 0.01 MPa or more, but from the viewpoint of foaming, it is limited to 1 MPa, and more preferably 0.5 MPa or less.

続いて、茶抽出液を大気圧以下の圧力にし、30秒〜20分間、好ましくは30秒〜10分間維持して安定化させる。大気圧以下の圧力下で維持することにより、溶液中に残存している酸素及び窒素が溶液外に発泡され、窒素混合した溶液が安定化する。これによって、製造された茶飲料における溶存酸素濃度やpHのバラツキの発生を減少させることができる。なお、この時、安定化時間が長すぎると、酸素の再溶解が生じる恐れがあるため、20分を目安とする。10分以下に留めると、より効果的に酸素の再溶解を抑えることが可能である。   Subsequently, the tea extract is brought to a pressure equal to or lower than atmospheric pressure, and is stabilized for 30 seconds to 20 minutes, preferably 30 seconds to 10 minutes. By maintaining the pressure below atmospheric pressure, oxygen and nitrogen remaining in the solution are foamed out of the solution, and the nitrogen mixed solution is stabilized. Thereby, generation | occurrence | production of the variation in dissolved oxygen concentration and pH in the manufactured tea drink can be reduced. At this time, if the stabilization time is too long, re-dissolution of oxygen may occur. If it is kept for 10 minutes or less, it is possible to suppress re-dissolution of oxygen more effectively.

さらに、安定化を行った茶抽出液のpHを再び調整する。本工程におけるpH調整では、香味、色調の劣化を抑える観点から、pH5.5〜6.5の範囲に調整するとよい。好ましくはpH5.8〜6.3に調整することによって、後に続く殺菌工程による香味、色調の劣化を最小限に抑えることが可能である。   Further, the pH of the stabilized tea extract is adjusted again. In pH adjustment in this process, it is good to adjust to the range of pH5.5-6.5 from a viewpoint of suppressing deterioration of a flavor and a color tone. Preferably, by adjusting the pH to 5.8 to 6.3, it is possible to minimize the deterioration of flavor and color tone due to the subsequent sterilization process.

以上の工程によって調製された茶抽出液は、その溶存酸素量が通常1 ppm以下である。このようにして得られた茶抽出液は、続いて加熱殺菌され、密封容器に充填されて茶飲料製品として提供されることができる。   The tea extract prepared by the above steps usually has a dissolved oxygen content of 1 ppm or less. The tea extract thus obtained can be subsequently heat sterilized, filled in a sealed container and provided as a tea beverage product.

以上記載したように、本発明の方法に従うことにより、茶抽出液の溶存酸素濃度を安定的に低減することができ、窒素混合及び加熱殺菌による酸化劣化を確実に抑制することが可能である。よって、香味水色ともに優れた茶本来の風味を保持する茶飲料を安定的に提供することが可能である。   As described above, by following the method of the present invention, the dissolved oxygen concentration of the tea extract can be stably reduced, and the oxidative deterioration due to nitrogen mixing and heat sterilization can be reliably suppressed. Therefore, it is possible to stably provide a tea beverage that retains the original flavor of tea that is excellent in flavor and light blue.

なお、本発明の方法に従って製造された茶飲料は、PET、ビン、缶、紙パック等の何れの密封容器に充填されてもよく、特に、高バリアPETに充填されることが好ましいが、これらに限定されない。ここで、高バリアPETとは、樹脂を多層にしたり酸素吸収能力のある素材を挿入したりすることによって酸素の透過量を減じたPETを意味し、通常のPETよりも酸素透過量が少ないPETであれば何れのものであってもよい。   The tea beverage produced according to the method of the present invention may be filled in any sealed container such as PET, bottles, cans, paper packs and the like, and particularly preferably filled in high barrier PET. It is not limited to. Here, the high barrier PET means PET in which the amount of permeated oxygen is reduced by making the resin into a multilayer or inserting a material capable of absorbing oxygen, and has a smaller amount of oxygen permeation than normal PET. Any one may be used.

次に、本発明の方法に従って茶飲料を調製し官能評価を行った。各実施例及び比較例の茶飲料の調製方法は、以下に詳細に示した。   Next, a tea beverage was prepared according to the method of the present invention and sensory evaluation was performed. The methods for preparing the tea beverages of each Example and Comparative Example are shown in detail below.

[実施例1]
緑茶葉100gを85℃で4分間抽出した後、茶葉を分離して25℃に冷却し、次いで濾過して清澄化させた。この抽出液にアスコルビン酸(BASF武田ビタミン株式会社)3gを添加し、重曹を用いてpHを5.7に調整した調合液10kgを得た。
この調合液をガス置換方式にて窒素混合した後、0.04 MPaの負圧を加え、続いて大気圧下で7分間保持し、安定化させるとともにアスコルビン酸にてpHを6.2に補正した。この時の溶存酸素濃度は0.2 ppmであった。
その後、136℃で30秒間殺菌し、PETボトルに充填して容器詰緑茶飲料とした。
[Example 1]
After extracting 100 g of green tea leaves at 85 ° C. for 4 minutes, the tea leaves were separated and cooled to 25 ° C. and then clarified by filtration. To this extract, 3 g of ascorbic acid (BASF Takeda Vitamin Co., Ltd.) was added, and 10 kg of a prepared solution with pH adjusted to 5.7 using sodium bicarbonate was obtained.
After this mixed solution was mixed with nitrogen by a gas replacement method, a negative pressure of 0.04 MPa was applied, and then kept at atmospheric pressure for 7 minutes to stabilize and correct the pH to 6.2 with ascorbic acid. The dissolved oxygen concentration at this time was 0.2 ppm.
Thereafter, it was sterilized at 136 ° C. for 30 seconds and filled into a PET bottle to obtain a container-packed green tea beverage.

[実施例2]
緑茶葉100gを85℃で4分間抽出した後、茶葉を分離して25℃に冷却し、次いで濾過して清澄化させた。この抽出液にアスコルビン酸(BASF武田ビタミン株式会社)3gを添加し、重曹を用いてpHを5.6に調整した調合液10kgを得た。
この調合液をガス置換方式にて窒素混合した後、0.03 MPaの負圧を加え、続いて大気圧下で1分間保持し、安定化させるとともにアスコルビン酸にてpHを6.1に補正した。この時の溶存酸素濃度は0.3 ppmであった。
その後、136℃で30秒間殺菌し、PETボトルに充填して容器詰緑茶飲料とした。
[Example 2]
After extracting 100 g of green tea leaves at 85 ° C. for 4 minutes, the tea leaves were separated and cooled to 25 ° C. and then clarified by filtration. To this extract, 3 g of ascorbic acid (BASF Takeda Vitamin Co., Ltd.) was added, and 10 kg of a prepared solution with pH adjusted to 5.6 using sodium bicarbonate was obtained.
After this mixed solution was mixed with nitrogen by a gas replacement method, a negative pressure of 0.03 MPa was applied, and then kept at atmospheric pressure for 1 minute to stabilize and the pH was corrected to 6.1 with ascorbic acid. The dissolved oxygen concentration at this time was 0.3 ppm.
Thereafter, it was sterilized at 136 ° C. for 30 seconds and filled into a PET bottle to obtain a container-packed green tea beverage.

[実施例3]
緑茶葉100gを85℃で4分間抽出した後、茶葉を分離して25℃に冷却し、次いで濾過して清澄化させた。この抽出液にアスコルビン酸(BASF武田ビタミン株式会社)3gを添加し、重曹を用いてpHを5.7に調整した調合液10kgを得た。
この調合液をガス置換方式にて窒素混合した後、0.04 MPaの負圧を加え、続いて大気圧下で2分間保持し、安定化させた後、アスコルビン酸にてpHを6.2に補正した。この時の溶存酸素濃度は0.3 ppmであった。
その後、136℃で30秒間殺菌し、無菌条件下にて殺菌済みPETボトルに充填して容器詰緑茶飲料とした。
[Example 3]
After extracting 100 g of green tea leaves at 85 ° C. for 4 minutes, the tea leaves were separated and cooled to 25 ° C. and then clarified by filtration. To this extract, 3 g of ascorbic acid (BASF Takeda Vitamin Co., Ltd.) was added, and 10 kg of a prepared solution with pH adjusted to 5.7 using sodium bicarbonate was obtained.
After this mixed solution was mixed with nitrogen by a gas replacement method, a negative pressure of 0.04 MPa was applied, and subsequently maintained at atmospheric pressure for 2 minutes to stabilize, and then the pH was corrected to 6.2 with ascorbic acid. The dissolved oxygen concentration at this time was 0.3 ppm.
Thereafter, it was sterilized at 136 ° C. for 30 seconds and filled in a sterilized PET bottle under aseptic conditions to obtain a container-packed green tea beverage.

[実施例4]
実施例1の方法で殺菌まで行い、高バリアボトル(北海製罐株式会社製アクティスボトル)に充填し容器詰緑茶飲料とした。
[Example 4]
Sterilization was performed by the method of Example 1, filled into a high barrier bottle (Aktis bottle manufactured by Hokkai Seikan Co., Ltd.) to obtain a container-packed green tea beverage.

[比較例1]
緑茶葉100gを85℃で4分間抽出した後、茶葉を分離して25℃に冷却し、次いで濾過して清澄化させた。この抽出液にアスコルビン酸(BASF武田ビタミン株式会社)3gを添加し、重曹を用いてpHを6.3に調整した調合液10kgを得た。この時の溶存酸素濃度は7.2 ppmであった。
この調合液をガス置換方式にて窒素混合した後、0.05 MPaの負圧を加え、続いて大気圧下で3分間保持した。この時の溶存酸素濃度は0.3 ppmであった。
その後、136℃で30秒間殺菌し、PETボトルに充填して容器詰緑茶飲料とした。
[Comparative Example 1]
After extracting 100 g of green tea leaves at 85 ° C. for 4 minutes, the tea leaves were separated and cooled to 25 ° C. and then clarified by filtration. To this extract, 3 g of ascorbic acid (BASF Takeda Vitamin Co., Ltd.) was added, and 10 kg of a prepared solution with pH adjusted to 6.3 using sodium bicarbonate was obtained. The dissolved oxygen concentration at this time was 7.2 ppm.
After this mixed solution was mixed with nitrogen by a gas replacement method, a negative pressure of 0.05 MPa was applied, and then maintained at atmospheric pressure for 3 minutes. The dissolved oxygen concentration at this time was 0.3 ppm.
Thereafter, it was sterilized at 136 ° C. for 30 seconds and filled into a PET bottle to obtain a container-packed green tea beverage.

[比較例2]
緑茶葉100gを85℃で4分間抽出した後、茶葉を分離して25℃に冷却し、次いで濾過して清澄化させた。この抽出液にアスコルビン酸(BASF武田ビタミン株式会社)3gを添加し、重曹を用いてpHを4.6に調整した調合液10kgを得た。この時の溶存酸素濃度は7.5 ppmであった。
この調合液をガス置換方式にて窒素混合した後、0.05 MPaの負圧を加え、続いて大気圧下で3分間保持した。この時の溶存酸素濃度は0.3 ppmであった。
[Comparative Example 2]
After extracting 100 g of green tea leaves at 85 ° C. for 4 minutes, the tea leaves were separated and cooled to 25 ° C. and then clarified by filtration. To this extract, 3 g of ascorbic acid (BASF Takeda Vitamin Co., Ltd.) was added, and 10 kg of a prepared solution with pH adjusted to 4.6 using sodium bicarbonate was obtained. The dissolved oxygen concentration at this time was 7.5 ppm.
After this mixed solution was mixed with nitrogen by a gas replacement method, a negative pressure of 0.05 MPa was applied, and then maintained at atmospheric pressure for 3 minutes. The dissolved oxygen concentration at this time was 0.3 ppm.

その後、136℃で30秒間殺菌し、PETボトルに充填して容器詰緑茶飲料とした。   Thereafter, it was sterilized at 136 ° C. for 30 seconds and filled into a PET bottle to obtain a container-packed green tea beverage.

[比較例3]
緑茶葉100gを85℃で4分間抽出した後、茶葉を分離して25℃に冷却し、次いで濾過して清澄化させた。この抽出液にアスコルビン酸(BASF武田ビタミン株式会社)3gを添加し、重曹を用いてpHを6.2に調整した調合液10kgを得た。この時の溶存酸素濃度は7.6 ppmであった。
その後、136℃で30秒間殺菌し、PETボトルに充填して容器詰緑茶飲料とした。
[Comparative Example 3]
After extracting 100 g of green tea leaves at 85 ° C. for 4 minutes, the tea leaves were separated and cooled to 25 ° C. and then clarified by filtration. To this extract, 3 g of ascorbic acid (BASF Takeda Vitamin Co., Ltd.) was added, and 10 kg of a prepared solution with pH adjusted to 6.2 using sodium bicarbonate was obtained. The dissolved oxygen concentration at this time was 7.6 ppm.
Thereafter, it was sterilized at 136 ° C. for 30 seconds and filled into a PET bottle to obtain a container-packed green tea beverage.

[比較例4]
緑茶葉100gを85℃で4分間抽出した後、茶葉を分離して25℃に冷却し、次いで濾過して清澄化させた。この抽出液にアスコルビン酸(BASF武田ビタミン株式会社)3gを添加し、重曹を用いてpHを5.7に調整した調合液10kgを得た。この時の溶存酸素濃度は7.6 ppmであった。
この調合液をガス置換方式にて窒素混合した後、大気圧に4分間保持させ安定化させると共に、アスコルビン酸にてpHを6.1に補正した。この時の溶存酸素濃度は1.8 ppmであった。
その後、136℃で30秒間殺菌し、PETボトルに充填して容器詰緑茶飲料とした。
[Comparative Example 4]
After extracting 100 g of green tea leaves at 85 ° C. for 4 minutes, the tea leaves were separated and cooled to 25 ° C. and then clarified by filtration. To this extract, 3 g of ascorbic acid (BASF Takeda Vitamin Co., Ltd.) was added, and 10 kg of a prepared solution with pH adjusted to 5.7 using sodium bicarbonate was obtained. The dissolved oxygen concentration at this time was 7.6 ppm.
After this mixed solution was mixed with nitrogen by a gas replacement method, it was kept at atmospheric pressure for 4 minutes for stabilization, and the pH was corrected to 6.1 with ascorbic acid. The dissolved oxygen concentration at this time was 1.8 ppm.
Thereafter, it was sterilized at 136 ° C. for 30 seconds and filled into a PET bottle to obtain a container-packed green tea beverage.

[比較例5]
緑茶葉100gを85℃で4分間抽出した後、茶葉を分離して25℃に冷却し、次いで濾過して清澄化させた。この抽出液にアスコルビン酸(BASF武田ビタミン株式会社)3gを添加し、重曹を用いてpHを5.7に調整した調合液10kgを得た。この時の溶存酸素濃度は7.6 ppmであった。
この調合液をガス置換方式にて窒素混合した後、0.04 MPaの負圧を加え、大気圧下で保持せずに136℃で30秒間殺菌し、PETボトルに充填して容器詰緑茶飲料とした。
[Comparative Example 5]
After extracting 100 g of green tea leaves at 85 ° C. for 4 minutes, the tea leaves were separated and cooled to 25 ° C. and then clarified by filtration. To this extract, 3 g of ascorbic acid (BASF Takeda Vitamin Co., Ltd.) was added, and 10 kg of a prepared solution with pH adjusted to 5.7 using sodium bicarbonate was obtained. The dissolved oxygen concentration at this time was 7.6 ppm.
This mixed solution was mixed with nitrogen by a gas replacement method, then a negative pressure of 0.04 MPa was applied, sterilized at 136 ° C. for 30 seconds without being kept under atmospheric pressure, filled into a PET bottle and made into a container-packed green tea beverage .

[比較例6]
緑茶葉100gを85℃で4分間抽出した後、茶葉を分離して25℃に冷却し、次いで濾過して清澄化させた。この抽出液にアスコルビン酸(BASF武田ビタミン株式会社)3gを添加し、重曹を用いてpHを5.6に調整した調合液10kgを得た。この時の溶存酸素濃度は7.8 ppmであった。
この調合液をガス置換方式にて窒素混合した後、0.05 MPaの負圧を加え、続いて大気圧で30分間保持し安定化させると共に、アスコルビン酸にてpHを6.2に補正した。この時の溶存酸素濃度は1.7 ppmであった。
その後、136℃で30秒間殺菌し、PETボトルに充填して容器詰緑茶飲料とした。
[Comparative Example 6]
After extracting 100 g of green tea leaves at 85 ° C. for 4 minutes, the tea leaves were separated and cooled to 25 ° C. and then clarified by filtration. To this extract, 3 g of ascorbic acid (BASF Takeda Vitamin Co., Ltd.) was added, and 10 kg of a prepared solution with pH adjusted to 5.6 using sodium bicarbonate was obtained. The dissolved oxygen concentration at this time was 7.8 ppm.
This mixed solution was mixed with nitrogen by a gas replacement method, and then a negative pressure of 0.05 MPa was applied. Subsequently, the mixture was maintained at atmospheric pressure for 30 minutes for stabilization, and the pH was corrected to 6.2 with ascorbic acid. The dissolved oxygen concentration at this time was 1.7 ppm.
Thereafter, it was sterilized at 136 ° C. for 30 seconds and filled into a PET bottle to obtain a container-packed green tea beverage.

[比較例7]
緑茶葉100gを85℃で4分間抽出した後、茶葉を分離して25℃に冷却し、次いで濾過して清澄化させた。この抽出液にアスコルビン酸(BASF武田ビタミン株式会社)3gを添加し、重曹を用いてpHを5.8に調整した調合液10kgを得た。この時の溶存酸素濃度は7.6 ppmであった。
この調合液をガス置換方式にて窒素混合した後、136℃で30秒間殺菌し、PETボトルに充填して容器詰緑茶飲料とした。
[Comparative Example 7]
After extracting 100 g of green tea leaves at 85 ° C. for 4 minutes, the tea leaves were separated and cooled to 25 ° C. and then clarified by filtration. To this extract, 3 g of ascorbic acid (BASF Takeda Vitamin Co., Ltd.) was added, and 10 kg of a prepared solution with pH adjusted to 5.8 using sodium bicarbonate was obtained. The dissolved oxygen concentration at this time was 7.6 ppm.
This mixed solution was mixed with nitrogen by a gas replacement method, sterilized at 136 ° C. for 30 seconds, and filled into a PET bottle to obtain a container-packed green tea beverage.

[比較例8]
緑茶葉100gを85℃で4分間抽出した後、茶葉を分離して25℃に冷却し、次いで濾過して清澄化させた。この抽出液にアスコルビン酸(BASF武田ビタミン株式会社)3gを添加し、重曹を用いてpHを6.0に調整した調合液10kgを得た。この時の溶存酸素濃度は7.4 ppmであった。
この調合液を真空脱気方式にて脱気処理し溶存酸素濃度を3.6 ppmまで低下させ136℃で30秒間殺菌し、PETボトルに充填して容器詰緑茶飲料とした。
[Comparative Example 8]
After extracting 100 g of green tea leaves at 85 ° C. for 4 minutes, the tea leaves were separated and cooled to 25 ° C. and then clarified by filtration. To this extract, 3 g of ascorbic acid (BASF Takeda Vitamin Co., Ltd.) was added, and 10 kg of a prepared solution adjusted to pH 6.0 with sodium bicarbonate was obtained. The dissolved oxygen concentration at this time was 7.4 ppm.
This prepared solution was deaerated by a vacuum deaeration method to reduce the dissolved oxygen concentration to 3.6 ppm, sterilized at 136 ° C. for 30 seconds, filled into a PET bottle, and made into a container-packed green tea beverage.

[結果]
実施例及び比較例の緑茶飲料を、製造直後、及び37℃で2週間保管した後に官能評価した。製造直後の茶飲料の評価を1次評価、37℃で2週間保管した茶飲料の評価を2次評価と称し、それぞれの結果を表1に示した。なお、官能評価は5人の熟練した審査官により行い、評価基準は次の通りである; 良好:4点、やや良好:3点、やや悪い:2点、悪い:1点。また、総合評価として、5人の平均点を次のように記載した; ◎:3.5以上、 〇:2.5以上、 △:1.5以上2.5未満、 ×:1.5未満。

Figure 0004411250
[result]
The green tea beverages of Examples and Comparative Examples were subjected to sensory evaluation immediately after production and after storage at 37 ° C. for 2 weeks. Evaluation of the tea beverage immediately after production was referred to as primary evaluation, and evaluation of the tea beverage stored at 37 ° C. for 2 weeks was referred to as secondary evaluation. The results are shown in Table 1. The sensory evaluation was performed by five skilled examiners, and the evaluation criteria are as follows: Good: 4 points, slightly good: 3 points, slightly bad: 2 points, bad: 1 point. In addition, as a comprehensive evaluation, the average score of five people was described as follows: ◎: 3.5 or more, ○: 2.5 or more, △: 1.5 or more and less than 2.5, ×: less than 1.5.
Figure 0004411250

比較例1は、味が淡白で特に水色の褐変が生じた。また、比較例2は、イモ様の香気が生じた。比較例1・2はともに、pHが本発明による適正範囲外であり、よって、pHの調整が不十分であることにより風味に影響が及ぼされることが示された。
比較例3は、香気が弱く味の劣化臭および水色の褐変がみられた。これは、窒素混合を行わなかったことによるものと考えられる。比較例4は、窒素混合を行ったが、負圧を加える工程を行わなかった為に窒素置換が不十分であることが示された。
安定化工程を行わなかった比較例5は、香りが弱く水色が褐変傾向になった。また、比較例7は、窒素混合を行ったが、負圧を加える工程及び安定化工程を行わなかった。この比較例7では、香りが弱く水色の褐変が生じた。これらに対して、略同じ条件の実施例3は、香り、水色ともに優れており、負圧・安定化工程によって窒素置換が効率よく行われることが示された。
比較例6は、香気、水色ともにやや劣化しており、安定化工程が長かったために酸素の再溶存が起こったものと考えられる。
In Comparative Example 1, the taste was light white and particularly light blue browning occurred. Moreover, the comparative example 2 produced the potato-like aroma. In both Comparative Examples 1 and 2, it was shown that the pH is outside the appropriate range according to the present invention, and therefore the flavor is affected by insufficient pH adjustment.
In Comparative Example 3, the fragrance was weak, and the taste-deteriorating odor and light blue browning were observed. This is considered due to the fact that nitrogen mixing was not performed. Although the comparative example 4 performed nitrogen mixing, since the process of applying a negative pressure was not performed, it was shown that nitrogen substitution is inadequate.
In Comparative Example 5 in which the stabilization process was not performed, the fragrance was weak and the light blue color turned brown. Moreover, although the comparative example 7 performed nitrogen mixing, the process of adding a negative pressure and the stabilization process were not performed. In Comparative Example 7, the fragrance was weak and light blue browning occurred. On the other hand, Example 3 under substantially the same conditions was excellent in both fragrance and light blue color, and it was shown that nitrogen substitution was efficiently performed by the negative pressure / stabilization process.
In Comparative Example 6, both the aroma and light blue were slightly deteriorated, and it is considered that re-dissolution of oxygen occurred because the stabilization process was long.

比較例8は、脱気操作を行ったが、香りの評価が極めて低く、脱気操作によって香りが抜けることが示された。
一方、本発明に従って窒素を混合し、その後負圧を加える工程、安定化工程、及びpH調整を行った実施例1・2・3・4は、ともに良好な結果が得られた。実施例4では高バリアボトルの使用により2次評価で顕著な効果がみられ特に良好であった。
In Comparative Example 8, the deaeration operation was performed, but the evaluation of the scent was extremely low, and it was shown that the scent was removed by the deaeration operation.
On the other hand, good results were obtained in Examples 1, 2, 3, and 4 in which nitrogen was mixed in accordance with the present invention, and then the negative pressure was applied, the stabilization step, and the pH adjusted. In Example 4, the use of the high barrier bottle showed a remarkable effect in the secondary evaluation and was particularly good.

Claims (6)

茶葉を抽出し、得られた茶抽出液をpH5.0〜6.0に調整する工程と、
該茶抽出液に窒素を混合し、さらに0.01 MPa以上の負圧を加える工程と、
前記負圧を加える工程に続いて、該茶抽出液を大気圧以下の圧力下で30秒〜20分間維持し、安定化させる工程と、
前記安定化工程中又は該工程後に、該茶抽出液をpH5.5〜6.5に調整する工程と、
を具備する、茶飲料の製造方法。
Extracting tea leaves and adjusting the resulting tea extract to pH 5.0-6.0;
Mixing the tea extract with nitrogen and further applying a negative pressure of 0.01 MPa or more;
Following the step of applying the negative pressure, maintaining the tea extract at a pressure below atmospheric pressure for 30 seconds to 20 minutes to stabilize,
Adjusting the tea extract to pH 5.5-6.5 during or after the stabilization step;
A method for producing a tea beverage, comprising:
前記安定化工程後にpHを調整された茶抽出液は、溶存酸素量が1 ppm以下であることを特徴とする、請求項1に記載の茶飲料の製造方法。   The method for producing a tea beverage according to claim 1, wherein the tea extract whose pH is adjusted after the stabilizing step has a dissolved oxygen content of 1 ppm or less. 前記安定化工程は大気圧下で行われる、請求項1又は2に記載の茶飲料の製造方法。   The method for producing a tea beverage according to claim 1 or 2, wherein the stabilization step is performed under atmospheric pressure. 前記茶飲料を殺菌し、密封容器に充填する工程をさらに具備する、請求項1〜3の何れか一項に記載の茶飲料の製造方法。   The method for producing a tea beverage according to any one of claims 1 to 3, further comprising a step of sterilizing the tea beverage and filling a sealed container. 前記密封容器に充填する工程が無菌条件下で行われる、請求項4に記載の茶飲料の製造方法。   The method for producing a tea beverage according to claim 4, wherein the step of filling the sealed container is performed under aseptic conditions. 前記密封容器は、高バリアPETである、請求項1〜5の何れか一項に記載の茶飲料の
製造方法。
The said sealed container is a manufacturing method of the tea drink as described in any one of Claims 1-5 which is high barrier PET.
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